Comparison of Bubble Size Distributions Inferred from Acoustic, Optical Visualisation, and Laser Diffraction

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colloids

and interfaces

Article

Comparison of Bubble Size Distributions Inferred

from Acoustic, Optical Visualisation,

and Laser Di

ff

raction

Pratik D Desai1 _{, Woon Choon Ng}2_{, Michael J Hines}1_{, Yassir Riaz}3_{, Vaclav Tesar}4 and William B Zimmerman3,*

1 _{Perlemax Ltd., 318 Broad Lane, She}_ffi_{eld S3 7HQ, UK; [email protected] (P.D.D.);}

[email protected] (M.J.H.)

2 _{Department of Mechanical Engineering, Mappin Street, University of She}_ffi_{eld, She}_ffi_{eld S1 3JD, UK;}

[email protected]

3 _{Department of Chemical and Biological Engineering, Mappin Street, University of She}_ffi_eld,

Sheffield S1 3JD, UK; [email protected]

4 _{Institute of Thermomechanics v.v.i., Czech Academy of Sciences, Dolejškova 5,}

182 00 Praha-Kobylisy, Czech Republic; [email protected] * Correspondence: [email protected]

Received: 25 August 2019; Accepted: 28 November 2019; Published: 5 December 2019

Abstract:Bubble measurement has been widely discussed in the literature and comparison studies have been widely performed to validate the results obtained for various forms of bubble size inferences. This paper explores three methods used to obtain a bubble size distribution—optical detection, laser diffraction and acoustic inferences—for a bubble cloud. Each of these methods has advantages and disadvantages due to their intrinsic inference methodology or design flaws due to lack of specificity in measurement. It is clearly demonstrated that seeing bubbles and hearing them are substantially and quantitatively different. The main hypothesis being tested is that for a bubble cloud, acoustic methods are able to detect smaller bubbles compared to the other techniques, as acoustic measurements depend on an intrinsic bubble property, whereas photonics and optical methods are unable to “see” a smaller bubble that is behind a larger bubble. Acoustic methods provide a real-time size distribution for a bubble cloud, whereas for other techniques, appropriate adjustments or compromises must be made in order to arrive at robust data. Acoustic bubble spectrometry consistently records smaller bubbles that were not detected by the other techniques. The difference is largest for acoustic methods and optical methods, with size differences ranging from 5–79% in average bubble size. Differences in size between laser diffraction and optical methods ranged from 5–68%. The differences between laser diffraction and acoustic methods are less, and range between 0% (i.e., in agreement) up to 49%. There is a wider difference observed between the optical method, laser diffraction and acoustic methods whilst good agreement between laser diffraction and acoustic methods. The significant disagreement between laser diffraction and acoustic method (35% and 49%) demonstrates the hypothesis, as there is a higher proportion of smaller bubbles in these measurements (i.e., the smaller bubbles ‘hide’ during measurement via laser diffraction). This study, which shows that acoustic bubble spectrometry is able to detect smaller bubbles than laser diffraction and optical techniques. This is supported by heat and mass transfer studies that show enhanced performance due to increased interfacial area of microbubbles, compared to fine bubbles.

Keywords: microbubbles; fluidics; fluidic oscillation; acoustic bubble spectrometry; laser diffraction

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Colloids Interfaces2019,3, 65 2 of 20

1. Introduction

Bubble Visualisation Techniques

Bubbles ranging from (1µm–1000µm) in size are termed microbubbles. Although the actual definition of a microbubble depends on its application, for the purposes of this study, the aforementioned definition holds [1]. Bubbles have been visualised for over half a millennia with Newton’s observation of bubble formation with a pair of lenses, whilst the Berthelot tube method has long been known as a way to observe cavitation in liquids [2]. Reynolds discovered bubble formation by cavitation via the process of boiling [3]. Bubble visualisation is easier for fine bubbles or for sparse microbubbles generated by either energy intensive or low throughput methods. Single bubbles can be simply studied via a microscope or a lens. Characterising cloud bubble dynamics is more problematic. Common practice is to use optical imaging coupled with the volume fraction of the bubble by juxtaposing a control image (bubble-free) over the bubble cloud image, followed by using pixel data and a Hough transform to determine the void fraction. However, this does not necessarily provide any more information about the bubble size distribution (BSD). Therefore, optical methods were developed with algorithms relying on variety of techniques to estimate bubble sizes [4–11]. Interests in bubble cloud dynamics are largely focused on marine engineering and oceanic sciences. This is due to the high cost of producing microbubbles, thereby opposing the use of microbubbles for industrial purposes.

Fluidic oscillation offers substantial reduction in energy costs for generating microbubbles with concomitant increase of throughput [12]. The Tesaˇr–Zimmerman fluidic oscillator [13]—a modified version of the feedback loop type oscillator—made it possible to use microbubbles economically for industrial applications with several applications explored for lab-scale [14] and large-scale industrial purposes. Several T-Junction devices [15,16] and sonication [17], amongst other techniques can now be used for generating a cloud of microbubbles with a wide size distribution. With the advent of such techniques, the methods for visualisation have simultaneously shifted from direct measurement using a microscope to indirect techniques for higher accuracy through the exploitation of properties exhibited by bubbles. The BSD depend on the methods used for obtaining the bubble size and the statistical analyses that accompany these methods. Methods used for inferring BSD include four-point optical probe [18–21], capacitance probes [22], electrical conductivity [23], video imaging [24–27], acoustical backscatter [28], acoustic resonator [29], acoustic pulse propagation sensor [29], laser diffraction [30], acoustic attenuation [31–33], University of Capetown Technique (UCT) bubble size sampler [34] and laser attenuation [35].

Several comparison studies have been performed on bubble visualization, such as [5], as well as work on resolving optical and acoustic methods [29,36,37] in order to merge the understanding of these techniques and try to obtain a better understanding of these visualisation systems. However, comparison studies for cloud bubble dynamics with an emphasis on detecting smaller bubbles have not been performed, nor studied in detail.

Additionally, visual inspection, as can be seen in Figure1, show that for microbubble clouds, visual inferences cannot be made and size distributions need to be carefully obtained and analysed.

Statistical analyses performed on the sizing by each method skews the size distribution and therefore the final average bubble size obtained could be quite different depending on the actual statistical analysis applied. A comparison study is performed for three classes of bubble sizing techniques, including optical, laser diffraction, and acoustic. Specifically, Dynaflow’s Acoustic Bubble Spectrometer (ABS), Malvern Instruments’ SprayTec, and high-speed photography (Photron FastCam S3). Each method offers its own advantages and disadvantages depending on the actual method of estimating the bubble size population.

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This section discusses the distinct advantages offered by the different visualisation methods and other capabilities.

Colloids Interfaces 2018, 2, x FOR PEER REVIEW 3 of 20

This section discusses the distinct advantages offered by the different visualisation methods and other capabilities.

Figure 1. Photographic Visualisation of Cloud Bubble Dynamics (left) – control/steady flow, (right) oscillatory flow. Nothing significant can be inferred visually—the major problem when characterising microbubble clouds.

2. Optical Methods

This is a direct form of measurement and visualisation, as well as the simplest method since it is a quick and easy way to infer the BSD.

High-Speed Photography

Optical methods usually involve a monochromatic light source and require the liquid to be transparent to light. The greater the contrast between the bubble and the background, the more robust it is for automated image analysis. High-speed photography is commonly used due to its ease of use. Most high-speed cameras have the ability to capture more than 500 frames per second (fps).

The bubble generator is placed in the centre with the light source and the camera placed opposite each other in order to obtain the best contrast for the bubbles. Automated image analysis is made easier if there is a good contrast between the background and the bubbles. The camera need not be able to capture more than 2000 fps to obtain a BSD. The simplicity of the system is one of its key advantages and significantly reduces the costs of the system. Automated image analysis is possible by simple algorithms by using any suitable programming language viz. Octave, ImageJ, MATLAB, Mathematica, and LabView.

Image analysis can also be performed manually. It can, therefore, provide bubble sizes without the need of computing power (albeit a cumbersome approach). Although this technique is convenient for single bubbles, cloud bubble dynamics present their own drawbacks. Automated image analysis cannot be reliably used for overlapping bubbles, noncircular bubbles, and near-wall bubbles (the bubbles also need to be in a single plane). Depending on the angle used, the bubble size obtained is significantly different. A long working focal length lens could be used (to ensure wall effects are minimised) but makes the process more expensive and cumbersome.

This problem can be solved by using multiple cameras at the three focal planes but results in the need to develop a way to accrue synchronised information from the three cameras and then collate the information together in order to obtain a bubble spectrum. Bubbles at the wall, partial bubbles, noncircular (spherical for the 3D system) are not detected by automated image analysis. These features makes the task tedious and cumbersome, while introducing inference errors.

Different lenses are required for a particular size range. They cannot be used simultaneously unless another camera is used. A comprehensive BSD is therefore difficult to obtain, so only a certain size range is observed at a given time. Once the appropriate lens has been chosen and the camera focused, it cannot detect the other bubble size ranges and cannot differentiate between the particles and bubbles if they are too small. Multiple lenses increase the cost of the system, the number of measurements, and the required analyses and comparisons.

A number of additional analyses can be made using a high-speed camera. If the camera has a high frame rate, such as the Photron FastCam S3, the rise velocity of the bubble can be measured as

Figure 1. Photographic Visualisation of Cloud Bubble Dynamics (left)–control/steady flow, (right) oscillatory flow. Nothing significant can be inferred visually—the major problem when characterising microbubble clouds.

2. Optical Methods

This is a direct form of measurement and visualisation, as well as the simplest method since it is a quick and easy way to infer the BSD.

High-Speed Photography

Optical methods usually involve a monochromatic light source and require the liquid to be transparent to light. The greater the contrast between the bubble and the background, the more robust it is for automated image analysis. High-speed photography is commonly used due to its ease of use. Most high-speed cameras have the ability to capture more than 500 frames per second (fps).

The bubble generator is placed in the centre with the light source and the camera placed opposite each other in order to obtain the best contrast for the bubbles. Automated image analysis is made easier if there is a good contrast between the background and the bubbles. The camera need not be able to capture more than 2000fpsto obtain a BSD. The simplicity of the system is one of its key advantages and significantly reduces the costs of the system. Automated image analysis is possible by simple algorithms by using any suitable programming language viz. Octave, ImageJ, MATLAB, Mathematica, and LabView.

Image analysis can also be performed manually. It can, therefore, provide bubble sizes without the need of computing power (albeit a cumbersome approach). Although this technique is convenient for single bubbles, cloud bubble dynamics present their own drawbacks. Automated image analysis cannot be reliably used for overlapping bubbles, noncircular bubbles, and near-wall bubbles (the bubbles also need to be in a single plane). Depending on the angle used, the bubble size obtained is significantly different. A long working focal length lens could be used (to ensure wall effects are minimised) but makes the process more expensive and cumbersome.

This problem can be solved by using multiple cameras at the three focal planes but results in the need to develop a way to accrue synchronised information from the three cameras and then collate the information together in order to obtain a bubble spectrum. Bubbles at the wall, partial bubbles, noncircular (spherical for the 3D system) are not detected by automated image analysis. These features makes the task tedious and cumbersome, while introducing inference errors.

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A number of additional analyses can be made using a high-speed camera. If the camera has a high frame rate, such as the Photron FastCam S3, the rise velocity of the bubble can be measured as well as bubble formation dynamics, growth dynamics, conjunction and coalescence. Adil et al. [38] presents image analysis techniques for the rise velocity of a system with an ordinary camera.

3. Acoustic Methods

Acoustic methods have been used for bubble sizing for almost half a century. Excellent reviews on bubble sizing using acoustic methods have been compiled [39]. Bubble acoustic responses include backscatter, attenuation, resonance and sound speed modulations in the medium [32]. This is made possible as a result of the substantial effect that a bubble has on the propagation of acoustic waves.

A significant advance to demonstrate acoustic determination of the bubble sizes for bubble clouds was made in 1989 [40].

The relationship between complex sound speed in a bubbly medium (cm), and bubble free sound speed (c0), is defined by

c2₀ c2m(f)

=1+c 2 0 π

Z ∞

0

an(a)

f_R2−_f2₊_i_δ_f2da (1)

ais the bubble radius(m),f is the insonant frequency (Hz),fRis the natural frequency of the bubble of sizea,n(a) is the bubble density function andδis bubble damping magnitude.

This relationship by itself can be used for obtaining bubble size. However, there is a loss in fidelity, which is why other methods have been adopted for development. This along with the relation:

c2₀ c2m(f)

=u(f)−_iv₍_f₎ ₍₂₎

whereu(f)is speed and phase speed (v(f)) is given by: c2₀

u(f) (3)

And attenuation constantαis given by:

α(f) =20log₁₀e 2πf v c0

!

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This combination provides the bubble with a resonant frequency at which to oscillate. According to the solution of the Rayleigh–Plesset equation, the linear response of the bubble under continuous insonation and its nonlinear response, along with oscillation, is a property that is observed only for bubbles (not particles). These properties make this method favoured due to its specificity.

Also, in the Rayleigh region, the insonation frequency is dependent on the sixth power of the radius thereby making it a highly specific method.

f ∝_r6_[₃_] ₍₅₎

Several authors [41–51] have used hydrophones to infer bubble size, deploying these different properties in order to obtain BSD for coated (polymeric shells/protein shells, liposomes) and uncoated (clear interface) bubbles.

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Acoustic Bubble Spectrometry (ABS) by Dynaflow

Acoustic bubble spectrometry (ABS), used in this study is based on an assumption known as the resonant bubble approximation (RBA). The system and the algorithm used for the bubble size measurement is described well by [53].

The main development made by Dynaflow is the algorithm based on constrained minimisation. A hydrophone is a microphone that can be used underwater. As sound travels much faster in water and attenuates slower than with air as the medium, the design of the hydrophone has to be modified accordingly by matching its acoustic impedance in water [3]. An equiresponsive hydrophone pair is used in this system with one utilised for generation and the other for the detection.

Microbubbles oscillate linearly upon ultrasonic insonation. If the mechanical index of the insonation ultrasound is high enough, the oscillations become nonlinear, increasing the specificity, hence more effective for sizing. The acoustic pressure has to be increased to be able to cause a nonlinear response and a compression or expansion, which results in the emissions of nonlinear signals and their respective harmonics of the transmitted signal. This also causes the acoustic impedance of the bubble to change with respect to water, improving the signal. This can be thought of as a contrast enhancing effect of the coating on a coated medical microbubble.

Initially the two hydrophones are placed opposite each other with the bubble generator placed in the centre. The transmitter insonates starting from a specific frequency and performs a frequency sweep. This signal may or may not be amplified depending on the conditions. Whilst the receiver amplifies the signal, the data obtained is then inverted by bespoke software provided by the company. A zero calibration reading is taken (P0- analogous to any spectroscopic method). The production of bubbles causes a change in pressure when the bubble cloud is insonated. This change is recorded by the transducers and compared to the zero calibration reading.

The ABS (Figure2) provides continuous, real time bubble size distribution that are extremely specific to bubbles. Using an optimised octophonic system (four pairs of hydrophones), a comprehensive size distribution, between 10µm and 2 mm. Void fractions of down to 3×₁₀−3_{[53], can be measured}

and verified whilst conducting this study.

Acoustic Bubble Spectrometry (ABS) by Dynaflow

Acoustic bubble spectrometry (ABS), used in this study is based on an assumption known as the

resonant bubble approximation (RBA). The system and the algorithm used for the bubble size

measurement is described well by [53].

The main development made by Dynaflow is the algorithm based on constrained minimisation.

A hydrophone is a microphone that can be used underwater. As sound travels much faster in water

and attenuates slower than with air as the medium, the design of the hydrophone has to be modified

accordingly by matching its acoustic impedance in water [3]. An equiresponsive hydrophone pair is

used in this system with one utilised for generation and the other for the detection.

Microbubbles oscillate linearly upon ultrasonic insonation. If the mechanical index of the

insonation ultrasound is high enough, the oscillations become nonlinear, increasing the specificity,

hence more effective for sizing. The acoustic pressure has to be increased to be able to cause a

nonlinear response and a compression or expansion, which results in the emissions of nonlinear

signals and their respective harmonics of the transmitted signal. This also causes the acoustic

impedance of the bubble to change with respect to water, improving the signal. This can be thought

of as a contrast enhancing effect of the coating on a coated medical microbubble.

Initially the two hydrophones are placed opposite each other with the bubble generator placed

in the centre. The transmitter insonates starting from a specific frequency and performs a frequency

sweep. This signal may or may not be amplified depending on the conditions. Whilst the receiver

amplifies the signal, the data obtained is then inverted by bespoke software provided by the

company. A zero calibration reading is taken (P

0

- analogous to any spectroscopic method). The

production of bubbles causes a change in pressure when the bubble cloud is insonated. This change

is recorded by the transducers and compared to the zero calibration reading.

The ABS (Figure 2) provides continuous, real time bubble size distribution that are extremely

specific to bubbles. Using an optimised octophonic system (four pairs of hydrophones), a

comprehensive size distribution, between 10 µm and 2 mm. Void fractions of down to 3 × 10

−3

_[53],

can be measured and verified whilst conducting this study.

Figure 2. Schematic of the acoustic bubble spectrometer system comprised of bubble generating system (and hydrophones), signal amplifier and data processing.

Skewed results are obtained if bubbles stick to the surface of the hydrophones. Since the

hydrophones need to be submerged in the liquid, even small imperfections act as large centres for

bubble coalescence. Therefore, the hydrophones need to be regularly wiped and cleaned using water

[54].

The distinct advantage of acoustic spectrometry over laser diffraction and optical methods is

that bubbles in liquids are more transparent to acoustic waves than to light waves [36].

ABS can also be used to measure the sound speed of the medium and therefore determine the

viscosity or density of the medium.

Figure 2.Schematic of the acoustic bubble spectrometer system comprised of bubble generating system (and hydrophones), signal amplifier and data processing.

Skewed results are obtained if bubbles stick to the surface of the hydrophones. Since the hydrophones need to be submerged in the liquid, even small imperfections act as large centres for bubble coalescence. Therefore, the hydrophones need to be regularly wiped and cleaned using water [54].

The distinct advantage of acoustic spectrometry over laser diffraction and optical methods is that bubbles in liquids are more transparent to acoustic waves than to light waves [36].

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4. Photonic Methods

Photonic methods are most commonly used in particle sizing aside from optical imaging. Photonic methods are incredibly effective in terms of accuracy and range of the size distributions for small samples. The accuracy of photonic methods reduces for bubbles relative to particles not only due to the immanent property of the bubble but also due to total internal reflection that occurs upon illumination (presuming particles are opaque). Bubble opacity is not high so that the diaphanous behaviour exhibited by the bubbles affects the laser diffraction and scattering. Particles and bubbles interact with light (and sound) in three ways: absorption, emission and scattering. Assuming that the particles are spherical, the intensity of the scatter is measured and the BSD is inferred using Mie theory (assuming a noninteracting bubble cloud population). The scatter is dependent on the size of the particles, whilst the intensity is dependent on the number of particles. A bubble can be thought of as a dielectric sphere. An air filled bubble, with water as a medium, fits into this category. Mie theory describes diffraction, refraction and reflection (internal and external). Diffraction cannot tell the difference between a particle and bubble since it is independent of particle properties. Conversely, refraction and reflection are dependent on the type of particle and its refractive index. The refractive index, however, is fairly difficult to measure effectively. When light passes through a particle with an angle of incidence=00, there is no change to the incident light. However, at all the other angles the three effects can be observed depending on the angle of incidence. Total internal reflection is observed for incident angles above the critical angle. Several devices used for particle sizing using photonic methods have been reviewed [30].

Malvern SprayTec

According to Malvern Instruments, SprayTec uses dynamic light scattering (DLS) as a principle, and has a range with the 300 mm lens) between 0.1–900µm (Dx(50): 0.5–600µm). The system measures droplet size distributions and requires the angular intensity of light scattered from a spray to be measured as it passes through a laser beam (based on transmittance and scattering). This scattering pattern is first recorded and then analysed using Fraunhofer and Mie scattering to yield a size distribution. Complete resolution of the size dispersion has been obtained through optimisation as well as using a patented multiple scattering algorithm ensuring up to 98% obscuration [55].

Figure3shows a schematic of the SprayTec system. Two lasers, with collimating optics, are placed opposite each other with the test cell placed in the centre so that a small area of interest is measured. This was a modification made to the original setup as the usual method for measurement is spraying it in the space between the two lasers. The receiving lens adjusts itself—a self-correcting calibration system for alignment, which is critical for this measurement technique, and accounts for major errors and inconsistencies. This has been taken into account by the manufacturer by incorporating a separate collimator and an auto alignment feature embedded.

The modification made here is to use a glass cell for bubble measurement while using a macro provided by Malvern Instruments to account for changes in refractive index.

Bubbles are droplets with the phases inverted. Therefore, the SprayTec can be used for bubble size measurements especially for obtaining high density BSD [13,56].

Cloud bubble sizing might be a difficult phenomenon for laser diffraction techniques since the bubbles diffract far more than a particle with possibility of total internal reflection in a bubble. Since this principle depends on light diffraction and not a property exhibited specifically by bubbles alone, it cannot differentiate between bubble or particle. It is also affected by the diffractions caused by bubbles and particles in its vicinity and therefore some bubbles might be ‘hidden’. Photonic methods depend on the liquid being transparent to the wavelength of light but need not be transparent in the visible region. This gives an advantage to the photo-acoustic methods over optical methods.

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insonation frequency is not as monodisperse). However, it is the inversion of the same ill-posed Fredholm integral that makes this problem difficult [57].Colloids Interfaces 2018, 2, x FOR PEER REVIEW 7 of 20

Figure 3. SprayTec schematic.

One of the simplest theories used in particle sizing through laser diffraction is the Fraunhofer approximation. This model predicts the scattering pattern that is created when a solid, opaque disc of a known size is passed through a laser beam. This means that it is imperative that the transmission of light through the particle is assumed to be zero. For a bubble, that never happens. This model is satisfactory for large particles (over 50-µm diameter) but it does not describe the scattering exactly. The Fraunhofer approximation is no longer used due to the assumptions, which do not necessarily hold true for particles. However, they do hold true for bubbles.

The particle is much larger than the wavelength of light employed. ISO 13320:2009defines this

as being greater than 40 times the wavelength of incident light (i.e., 25 µm when a He-Ne laser is used). The other approximation is that all sizes of particle scatter with equal efficiencies. That is not true, since bubbles scatter more than particles and a bubble is not opaque.

It is for the above reasons that Mie theory is utilised; all the particles are spherical. For bubbles smaller than 1 mm, this approximation holds and is also used for the RBA assumption used in the ABS.

However, refractive indices for the material, medium and the absorption part of the refractive index must be known or estimated. These can be estimated for most substances and for bubbles—a comparatively a simpler prospect. Work has been conducted to demonstrate that laser diffraction is not very effective for obtaining cloud BSD [5]. Statistical methods need to be discussed since they are used in conjunction with any indirect forms of bubble size measurement.

5. Statistical Analyses

Size distributions are expressed in terms of number averages (simple average based on the number of bubbles) and void fraction averages (based on the volume occupied by the bubbles).

In particle sizing, and bubble sizing by extension, there are several methods to represent the BSD. In the work presented herein, there are quite a few larger bubbles in the steady flow condition compared to the oscillatory flow condition. However, with regard to the bigger bubbles, more are produced by the steady flow, with a significant contribution to the BSD due to the effect of the volume on the average sizes. The volume of a larger bubble has a much higher weighting than the smaller bubble on gas throughput. Therefore, a bubble of 1 mm size has a 1000 times greater impact in terms of volumetric flowrate than a 100 µm bubble. This means that a thousand 100 µm bubbles would

Figure 3.SprayTec schematic.

One of the simplest theories used in particle sizing through laser diffraction is the Fraunhofer approximation. This model predicts the scattering pattern that is created when a solid, opaque disc of a known size is passed through a laser beam. This means that it is imperative that the transmission of light through the particle is assumed to be zero. For a bubble, that never happens. This model is satisfactory for large particles (over 50-µm diameter) but it does not describe the scattering exactly. The Fraunhofer approximation is no longer used due to the assumptions, which do not necessarily hold true for particles. However, they do hold true for bubbles.

The particle is much larger than the wavelength of light employed. ISO 13320:2009 defines this as being greater than 40 times the wavelength of incident light (i.e., 25µm when a He-Ne laser is used). The other approximation is that all sizes of particle scatter with equal efficiencies. That is not true, since bubbles scatter more than particles and a bubble is not opaque.

It is for the above reasons that Mie theory is utilised; all the particles are spherical. For bubbles smaller than 1 mm, this approximation holds and is also used for the RBA assumption used in the ABS.

However, refractive indices for the material, medium and the absorption part of the refractive index must be known or estimated. These can be estimated for most substances and for bubbles—a comparatively a simpler prospect. Work has been conducted to demonstrate that laser diffraction is not very effective for obtaining cloud BSD [5]. Statistical methods need to be discussed since they are used in conjunction with any indirect forms of bubble size measurement.

5. Statistical Analyses

Size distributions are expressed in terms of number averages (simple average based on the number of bubbles) and void fraction averages (based on the volume occupied by the bubbles).

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of volumetric flowrate than a 100µm bubble. This means that a thousand 100µm bubbles would need to be produced to have the same volume as that of a single 1 mm bubble resulting in a skewed BSD due to this. Consider 1000 bubbles each of diameters 1µm, 100µm, and 500µm. Their number contribution is the same whereas their volume contribution is much higher, as shown in Figure4. Colloids Interfaces 2018, 2, x FOR PEER REVIEW 8 of 20

need to be produced to have the same volume as that of a single 1 mm bubble resulting in a skewed BSD due to this. Consider 1000 bubbles each of diameters 1 µm, 100 µm, and 500 µm. Their number contribution is the same whereas their volume contribution is much higher, as shown in Figure 4.

Figure 4. Effect of volume contribution and number contribution onthe average bubble size.

Number mean is important when only the number of bubbles/particles is of interest. This is used when the number of bubbles is more important than obtaining the size (for example, applications such as dispersed air flotation and froth flotation). Differences in bubble size based on number mean and volume contribution has been described in the literature [58,59].

Average bubble sizes vary with the particular data set being observed and are equally dependent on the analysis. However, this is amplified due to the change in the bubble dynamics. Analysis of single-bubble generation would not be a problem since both the average sizing values are fairly close to each other since the variance is lower. However, for cloud bubble dynamics, these effects become prominent. When it comes to over 1 × 106_{–1 × 10}9_{bubbles, even with a narrower size distribution,} large variances in bubble sizes are observed, depending on which method is used. For mass and heat transfer, it would generally be more appropriate to use void fraction for average bubble size for large sample sizes. The analysis utilises certain statistics (moments) used for calculating the different types of diameters.

The volume mean diameter is known as D4,3, also known as the third moment. Similarly, the surface area mean diameter is known as D3,2—the Sauter Mean Diameter [30,59,60].

The Specific Surface Area is the total area of the particles divided by their total weight.

Percentiles have been commonly used in particle sizing that determine the portion of particles which lie below or above the said percentage.

Those used with particular emphasis are – Dx(10), Dx(50) and Dx(90).

These values are also used to calculate the span of a BSD, which is actually the width of the size distribution. This is done using

𝐷𝑥(90)– 𝐷𝑥(10)

𝐷𝑥(50)

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Percentiles become important in order to characterise the histogram and size distributions. All of these values can be found in the British Standard BS2955:1993 or the ISO 13320:2009.

6. Hypothesis

The hypothesis of this paper is that acoustic methods are most accurate for small microbubbles since they are specific to bubbles, they do not miss small bubbles (since they rely upon the RBA) and

Figure 4.Effect of volume contribution and number contribution on the average bubble size.

Number mean is important when only the number of bubbles/particles is of interest. This is used when the number of bubbles is more important than obtaining the size (for example, applications such as dispersed air flotation and froth flotation). Differences in bubble size based on number mean and volume contribution has been described in the literature [58,59].

Average bubble sizes vary with the particular data set being observed and are equally dependent on the analysis. However, this is amplified due to the change in the bubble dynamics. Analysis of single-bubble generation would not be a problem since both the average sizing values are fairly close to each other since the variance is lower. However, for cloud bubble dynamics, these effects become prominent. When it comes to over 1×₁₀6_–1×₁₀9_{bubbles, even with a narrower size distribution,}

large variances in bubble sizes are observed, depending on which method is used. For mass and heat transfer, it would generally be more appropriate to use void fraction for average bubble size for large sample sizes. The analysis utilises certain statistics (moments) used for calculating the different types of diameters.

The volume mean diameter is known as D4,3, also known as the third moment. Similarly, the surface area mean diameter is known as D3,2—the Sauter Mean Diameter [30,59,60].

The Specific Surface Area is the total area of the particles divided by their total weight.

Percentiles have been commonly used in particle sizing that determine the portion of particles which lie below or above the said percentage.

Those used with particular emphasis are–Dx(10), Dx(50) and Dx(90).

These values are also used to calculate the span of a BSD, which is actually the width of the size distribution. This is done using

Dx(90)–Dx(10)

Dx(50) (6)

Percentiles become important in order to characterise the histogram and size distributions. All of these values can be found in the British Standard BS2955:1993 or the ISO 13320:2009.

6. Hypothesis

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can also be used in particle based systems due to this property (they neglect particles). They can also be used holistically rather than taking small sample sizes.

Microbubble size distributions cannot be visually determined but need careful measurement and analysis in order to better characterise the system.

The use of the fluidic oscillator as a means of controlled microbubble generation mediated by frequency changes aids in testing the hypothesis as it generates microbubbles of different size distributions at various frequencies. The crux of the hypothesis lies in the smaller population of the bubbles in order to test whether they ‘hide’ among the larger ones, which can be achieved using the fluidic oscillator. Whilst larger bubbles are simple to generate, smaller bubbles generated with a ceramic sparger are not as simple unless noncoalescent media [61] or surfactants [62,63] are added, which affect the sizing and visualisation paradigms.

7. Methods and Materials

7.1. Sparger

Sintered alumina spargers (2µm average pore size, 2 off–50 cm2area), which produces a cloud of fine bubbles approximately 500µm in size under steady flow [58] is used as the sparger in this study. This sparger, when coupled with the fluidic oscillator, can generate down to 7µm in average bubble size (number average) [58].

7.2. Fluidic Oscillator (FO)

A fluidic oscillator [64] (FO) is coupled with the accompanying pneumatic setup, Malvern SprayTec, Acoustic Bubble Spectrometer (ABS), High Speed Visualisation Setup, and frequency analysis kit. The frequency of the oscillator determines the rate of bubble generation.

7.3. Frequency Measurement and Fast Fourier Transform

Impress G-1000 pressure transducers and ADXL335 accelerometers are used. Fast Fourier Transforms are workhorse algorithms in signal processing, converting a signal from one domain (time or space) and to the frequency domain (and the inverse). The associated power spectrum provides a facile estimate the frequency of the oscillatory flow from the fluidic oscillator. LabView was used to acquire the signal and process it.

7.4. Microbubble Generation Setup

The global flow rate (see Figure5) is controlled by a flow meter while an accelerometer is placed at one of the legs in order to record the frequency of the FO for maintenance of experimental conditions. A relatively high global flow rate is required in order for the FO to oscillate, but the bleed valves control the flow rate that the spargers receive. Two configurations generating ten frequency conditions for bubble formation are used in the FO–sparger combination.

Twelve averages were taken for the ABS, with four each for the optical and photonic method. There is less than 3% error in the readings estimated for the ABS and SprayTec, while the optical method has 5% error levels.

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can also be used in particle based systems due to this property (they neglect particles). They can also be used holistically rather than taking small sample sizes.

Microbubble size distributions cannot be visually determined but need careful measurement and analysis in order to better characterise the system.

The use of the fluidic oscillator as a means of controlled microbubble generation mediated by frequency changes aids in testing the hypothesis as it generates microbubbles of different size distributions at various frequencies. The crux of the hypothesis lies in the smaller population of the bubbles in order to test whether they ‘hide’ among the larger ones, which can be achieved using the fluidic oscillator. Whilst larger bubbles are simple to generate, smaller bubbles generated with a ceramic sparger are not as simple unless noncoalescent media [61] or surfactants [62,63] are added, which affect the sizing and visualisation paradigms.

7. Methods and Materials

7.1. Sparger

Sintered alumina spargers (2 µm average pore size, 2 off – 50 cm2_{area), which produces a cloud} of fine bubbles approximately 500 µm in size under steady flow [58] is used as the sparger in this study. This sparger, when coupled with the fluidic oscillator, can generate down to 7µm in average bubble size (number average) [58].

7.2. Fluidic Oscillator (FO)

A fluidic oscillator [64] (FO) is coupled with the accompanying pneumatic setup, Malvern SprayTec, Acoustic Bubble Spectrometer (ABS), High Speed Visualisation Setup, and frequency analysis kit. The frequency of the oscillator determines the rate of bubble generation.

7.3. Frequency Measurement and Fast Fourier Transform

Impress G-1000 pressure transducers and ADXL335 accelerometers are used. Fast Fourier Transforms are workhorse algorithms in signal processing, converting a signal from one domain (time or space) and to the frequency domain (and the inverse). The associated power spectrum provides a facile estimate the frequency of the oscillatory flow from the fluidic oscillator. LabView was used to acquire the signal and process it.

7.4. Microbubble Generation Setup

The global flow rate (see Figure 5) is controlled by a flow meter while an accelerometer is placed at one of the legs in order to record the frequency of the FO for maintenance of experimental conditions. A relatively high global flow rate is required in order for the FO to oscillate, but the bleed valves control the flow rate that the spargers receive. Two configurations generating ten frequency conditions for bubble formation are used in the FO–sparger combination.

Figure 5. Pneumatic setup for bubble generation.

Figure 5.Pneumatic setup for bubble generation.

7.5. Optical Methods–High-Speed Photography

The visualisation device (see Figure6) is a high-speed camera, (Photron FastCam S3) capable of 250,000fpswith a resolution of 1024×_{1024 and provided with a lens (Nikon Nikkor Lens, 1.8 D).}

The region of interest used was 1.764 cm3(this takes into account the different focal planes used in order to capture sufficient data).

A single plane is used, as the image analysis software is not designed for a cloud of bubbles. Desai et al. [58] is the only other significant work done on 3D cloud bubble dynamics, but no automated image analysis on a 3D bubble population has been developed yet except attempting to do so [7]. It was assumed that it would be an equiresponsive surface and that a single plane could be representative as a microcosm of the overall cloud dynamical system. The appropriateness of this assumption in representativeness is one area where errors in measurement are introduced.

The systemic conditions are kept constant as described in the bubble generating system section. Colloids Interfaces 2018, 2, x FOR PEER REVIEW 10 of 20

Twelve averages were taken for the ABS, with four each for the optical and photonic method. There is less than 3% error in the readings estimated for the ABS and SprayTec, while the optical method has 5% error levels.

Systemic conditions were kept as constant as possible whilst comparing the different characterisation methods in order to introduce the least amount of replication error as possible. Since each technique has their own drawbacks and advantages, slight variations to the actual methods were required. For example, photonic and optical (single camera systems) methods can only be used for a single plane to image accurately or in a small space, so extrapolations have to be made. The acoustic method can size the entire population, but the hydrophones require separate use for two equiresponsive diffusers. The equivalence of the double sparger/hydrophone system to a single sparger plume is the major replication assumption made.

7.5. Optical Methods–High-Speed Photography

The visualisation device (see Figure 6) is a high-speed camera, (Photron FastCam S3) capable of 250,000 fps with a resolution of 1024 × 1024 and provided with a lens (Nikon Nikkor Lens, 1.8 D). The region of interest used was 1.764 cm3_{(this takes into account the different focal planes used in order} to capture sufficient data).

A single plane is used, as the image analysis software is not designed for a cloud of bubbles. Desai et al [58] is the only other significant work done on 3D cloud bubble dynamics, but no automated image analysis on a 3D bubble population has been developed yet except attempting to do so [7]. It was assumed that it would be an equiresponsive surface and that a single plane could be representative as a microcosm of the overall cloud dynamical system. The appropriateness of this assumption in representativeness is one area where errors in measurement are introduced.

The systemic conditions are kept constant as described in the bubble generating system section.

Figure 6. Setup for optical methods comparison study.

7.6. Photonic Method–SprayTec

SprayTec (see Figure 7) images a small sampling window. Within this field of vision, the statistical homogeneity and stationarity assumptions are made: bubbles are being produced equally from all regions of the spargers and that surface imperfections are negligible. The uniformity of this

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7.6. Photonic Method–SprayTec

SprayTec (see Figure7) images a small sampling window. Within this field of vision, the statistical homogeneity and stationarity assumptions are made: bubbles are being produced equally from all regions of the spargers and that surface imperfections are negligible. The uniformity of this assumption is the same problem as observed for optical methods. The gamut of the bubble population is possible only for a small test cell in case of bubble generation. Usually it is not required when compared to a spray. The SprayTec is able to infer BSDs whilst automatically adjusting for the change in refractive index due to the addition of the test cell. For an example, see Figure8.

assumption is the same problem as observed for optical methods. The gamut of the bubble population is possible only for a small test cell in case of bubble generation. Usually it is not required when compared to a spray. The SprayTec is able to infer BSDs whilst automatically adjusting for the change in refractive index due to the addition of the test cell. For an example, see Figure 8.

Figure 7. SprayTec setup – addition of fluidic oscillator and sparger into the modified SprayTec system (see Figure 4 for the standard system).

Figure 8. Example of spectrum for SprayTec. The red line is the cumulative volume graph. The BSD is provided with volume frequency as a metric.

Figure 7.SprayTec setup–addition of fluidic oscillator and sparger into the modified SprayTec system (see Figure4for the standard system).

assumption is the same problem as observed for optical methods. The gamut of the bubble population is possible only for a small test cell in case of bubble generation. Usually it is not required when compared to a spray. The SprayTec is able to infer BSDs whilst automatically adjusting for the change in refractive index due to the addition of the test cell. For an example, see Figure 8.

Figure 7. SprayTec setup – addition of fluidic oscillator and sparger into the modified SprayTec system (see Figure 4 for the standard system).

Figure 8. Example of spectrum for SprayTec. The red line is the cumulative volume graph. The BSD is provided with volume frequency as a metric.

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The 300 mm lens was used with particulate refractive index set at 1+0.01I, dispersant refractive index set at 1.33. The particle density was 1.23 g/cm3_{with residual set at 2.15% for the data.}

The transmission measurement involves a spatial filtering of the collimated laser beam pre and post transmission through the bubble cloud. The spatial filter is the pinhole at the centre of the detector array. As well as being used to ensure the detector array, it is centred on the laser beam and also rejects any scattered light. This is important, as it removes backscatter for most cases. However, for high scatterers, such as bubbles, due to concentration effects, multiple scattering inevitably causes some light to be rescattered back to a near-zero scattering angle. The laser used in SprayTec is a 632.8 nm, 2mW helium-neon laser. The transmitter contains the He:Ne laser source which produces a collimated beam of 10 mm diameter with a wavelength of 632.8 nm.

The detectors (over 30 of them), with the use of high-efficiency spatial filtering, means the concentration calculation is reliable over a much wider concentration range than a method based on measuring total scattered energy. This method requires no calibration and is able to carry out bubble sizing in real time. The media set are water and air.

7.7. Acoustic Method–Acoustic Bubble Spectrometer (ABS)

The measurements involving the ABS used four pairs of hydrophones with resonant frequencies at 50 kHz, 150 kHz, 250 kHz and 500 kHz. This ensured that the entire gamut of the BSD could be observed. The hydrophones were placed opposite each other and the bubbles insonated by ultrasound. The frequency of insonation determines bubble size and attenuation provides the number of bubbles. The bubble sizes obtained are for the entire sparger and are near real time measurements. Figure9 shows the setup for the experiment with the ABS.

The 300 mm lens was used with particulate refractive index set at 1+0.01I, dispersant refractive index set at 1.33. The particle density was 1.23 g/cm3_{with residual set at 2.15% for the data.}

The transmission measurement involves a spatial filtering of the collimated laser beam pre and post transmission through the bubble cloud. The spatial filter is the pinhole at the centre of the detector array. As well as being used to ensure the detector array, it is centred on the laser beam and also rejects any scattered light. This is important, as it removes backscatter for most cases. However, for high scatterers, such as bubbles, due to concentration effects, multiple scattering inevitably causes some light to be rescattered back to a near-zero scattering angle. The laser used in SprayTec is a 632.8 nm, 2mW helium-neon laser. The transmitter contains the He:Ne laser source which produces a collimated beam of 10 mm diameter with a wavelength of 632.8 nm.

The detectors (over 30 of them), with the use of high-efficiency spatial filtering, means the concentration calculation is reliable over a much wider concentration range than a method based on measuring total scattered energy. This method requires no calibration and is able to carry out bubble sizing in real time. The media set are water and air.

7.7. Acoustic Method–Acoustic Bubble Spectrometer (ABS)

The measurements involving the ABS used four pairs of hydrophones with resonant frequencies at 50 kHz, 150 kHz, 250 kHz and 500 kHz. This ensured that the entire gamut of the BSD could be observed. The hydrophones were placed opposite each other and the bubbles insonated by ultrasound. The frequency of insonation determines bubble size and attenuation provides the number of bubbles. The bubble sizes obtained are for the entire sparger and are near real time measurements. Figure 9 shows the setup for the experiment with the ABS.

Figure 9. Setup for the ABS—addition of the fluidic oscillator to an octophonic ABS system (see Figure 2 for standard stereophonic ABS setup).

8.Results

A comparison is made on the bubble sizing with the three methods. To ensure repeatability of bubble sizes, the frequencies of oscillation was measured using accelerometers and a pressure transducer. Figure 10 and Figure 11 show the average bubble sizes estimated for the spargers at different FO frequencies at different configurations using the three visualisation methods.

Figure 9.Setup for the ABS—addition of the fluidic oscillator to an octophonic ABS system (see Figure2

for standard stereophonic ABS setup).

8. Results

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Colloids InterfacesColloids Interfaces 20192018,, 2, x FOR PEER REVIEW 3, 65 13 of 20 13 of 20

Figure 10. Average BUBBLE SIZES at different frequencies of bubble generation for different methods

( - ABS , - SprayTec, - optical methods ).

The acoustic method shows an average bubble size with smaller bubbles than the other methods. Even for conditions with the same average bubble size, their respective BSD is different.

Figure 11. Average bubble sizes at different frequencies of bubble generation for different methods (

- ABS , - SprayTec, - optical methods ).

Although the SprayTec seems to correlate well with the high-speed camera and the ABS, the average bubble sizes obtained by the ABS are lower. Substantial data is condensed into a single point, resulting in a loss of fidelity and understanding. The window used for bubble sizing also influences the determination of the bubble size. For ABS, the sizes obtained can be smaller if using a smaller acquisition window. Due to the number average calculations, the average bubble sizes become much smaller.

The major point to note is the region of interest (ROI) recorded for these systems (Optical ROI – 1.76 cm3_{, Photonic ROI – 2 cm}3_{, ABS ROI – 353 cm}3_{). Normalisation on ROI had to be carried out as} the optical method has a single plane of interest which also depends on the focal plane. The photonic method depends on the ‘width’ of the laser (6 mm) and the depth of the spray. Since the light diffracts and the sensors record it, it is the beam of light for which the spread is measured. This means that

Figure 10.Average BUBBLE SIZES at different frequencies of bubble generation for different methods

(